Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
298.20 | 0.9996 |
303.20 | 0.9996 |
308.20 | 0.9996 |
313.20 | 0.9996 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
298.20 | 0.1081 |
303.20 | 0.1081 |
308.20 | 0.1081 |
313.20 | 0.1081 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
298.15 | 0.9999 |
303.15 | 0.9860 |
308.15 | 0.9948 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
298.15 | 0.0245 |
303.15 | 0.0204 |
308.15 | 0.0303 |
Operational conditions:
Mass fraction of Water (2) - Liquid mixture 1 |
---|
0.0121 |
0.9987 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
293.15 | 0.1204 |
313.15 | 0.1651 |
303.15 | 0.1376 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
293.15 | 0.9988 |
313.15 | 0.9990 |
303.15 | 0.9988 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 1-Hexanol, 2-ethyl- (1) - Liquid |
---|---|
273.25 | 0.0797 |
298.15 | 1.905 |
311.15 | 4.0942 |
332.15 | 100.18 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
298.20 | 0.9996 |
303.20 | 0.9996 |
308.20 | 0.9996 |
313.20 | 0.9996 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
298.20 | 0.1081 |
303.20 | 0.1081 |
308.20 | 0.1081 |
313.20 | 0.1081 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
298.15 | 0.9999 |
303.15 | 0.9860 |
308.15 | 0.9948 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 1)
Temperature, K - Liquid mixture 1 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
298.15 | 0.0245 |
303.15 | 0.0204 |
308.15 | 0.0303 |
Operational conditions:
Mass fraction of Water (2) - Liquid mixture 1 |
---|
0.0121 |
0.9987 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 1 |
---|---|
293.15 | 0.1204 |
313.15 | 0.1651 |
303.15 | 0.1376 |
Operational condition: Pressure, kPa = 101 (Liquid mixture 2)
Temperature, K - Liquid mixture 2 | Mole fraction of Water (2) - Liquid mixture 2 |
---|---|
293.15 | 0.9988 |
313.15 | 0.9990 |
303.15 | 0.9988 |
Operational condition: Mole fraction = 0 (Liquid)
Temperature, K - Liquid | Henry's Law constant (molality scale), kPa*kg/mol of 1-Hexanol, 2-ethyl- (1) - Liquid |
---|---|
273.25 | 0.0797 |
298.15 | 1.905 |
311.15 | 4.0942 |
332.15 | 100.18 |